Treatment process of triflumizole pesticide production wastewater
A technology for treating process and producing wastewater, which is applied in water/sewage treatment, natural water treatment, flotation water/sewage treatment, etc. It can solve the problems of complex discharge wastewater treatment process, incomplete recovery of active ingredients, and imperfect treatment process, etc. , to achieve good flocculation effect, reduce cost input and short process cycle
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Embodiment 1
[0030] A kind of treatment process of fluconazole pesticide production wastewater
[0031] Include the following steps:
[0032] Step 1. Raise the temperature of fluconazole pesticide production wastewater to 125°C at a rate of 5°C / min, keep it warm for 2 hours, then raise the temperature to 245°C at a rate of 10°C / min, oxidize it for 2 hours, and use a concentration of 0.2mol / L The sodium hydroxide solution absorbs nitrogen and carbon dioxide decomposed by waste water to obtain pretreated waste water;
[0033] Step 2: React the pretreated wastewater obtained in Step 1 in an iron-carbon reactor for 40 minutes, add flocculant to the discharged wastewater after the reaction, settle for 30 minutes, and filter the upper layer of wastewater;
[0034] Above, in the iron-carbon reactor: the iron content is 79%, the carbon content is 18%, and the palladium catalyst is 3%; the ratio of the flocculant to the pretreated wastewater is 10kg: 50L; the flocculant is composed of polyaluminum...
Embodiment 2
[0040] A kind of treatment process of fluconazole pesticide production wastewater
[0041] Include the following steps:
[0042] Step 1. Raise the temperature of fluconazole pesticide production wastewater to 135°C at a rate of 10°C / min, keep it warm for 3 hours, then raise the temperature to 285°C at a rate of 20°C / min, oxidize it for 4 hours, and use a concentration of 0.5mol / L The sodium hydroxide solution absorbs nitrogen and carbon dioxide decomposed by waste water to obtain pretreated waste water;
[0043] In step 2, the pretreated wastewater obtained in step 1 is reacted in an iron-carbon reactor for 55 minutes, and a flocculant is added to the discharged wastewater after the reaction, and after settling for 60 minutes, the upper layer of wastewater is filtered;
[0044]Above, in the iron-carbon reactor: the iron content is 83%, the carbon content is 14%, and the palladium catalyst is 3%; the ratio of the flocculant to the pretreated wastewater is 10kg: 60L; the floccu...
Embodiment 3
[0050] A kind of treatment process of fluconazole pesticide production wastewater
[0051] Include the following steps:
[0052] Step 1. Raise the temperature of fluconazole pesticide production wastewater to 127°C at a rate of 6°C / min, keep it warm for 3 hours, then raise the temperature to 255°C at a rate of 12°C / min, oxidize it for 4 hours, and use a concentration of 0.3mol / L The sodium hydroxide solution absorbs nitrogen and carbon dioxide decomposed by waste water to obtain pretreated waste water;
[0053] In step 2, the pretreated wastewater obtained in step 1 is reacted in an iron-carbon reactor for 45 minutes, and after the reaction, a flocculant is added to the discharged wastewater, and after settling for 40 minutes, the upper layer of wastewater is filtered;
[0054] Above, in the iron-carbon reactor: the iron content is 80%, the carbon content is 15%, and the palladium catalyst is 5%; the ratio of the flocculant to the pretreated wastewater is 10kg: 60L; the flocc...
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